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Process Equipment and Plant Design

Process Equipment and Plant Design
With increase in the number of shell passes, the value of FT

Remains same, only if the number of tube passes does not change
Increases
Remains same
Decreases

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Process Equipment and Plant Design
Tube side heat transfer co-efficient for turbulent flow of liquid through tubes is proportional to

G0.8
G0.5
G0.2
G1.5

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Process Equipment and Plant Design
For high pressure process equipments/vessels, the connected nozzle should be

Flanged
Welded
Brazed
Screwed

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Process Equipment and Plant Design
Minimum tube pitch recommended for shell and tube heat exchangers is about __________ times the outside diameter of the tube.

2.5
1.75
1.25
3.5

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Process Equipment and Plant Design
In case of a 'thin' pressure vessel, the ratio of its diameter to wall thickness is

> 20
> 10
30
< 10

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Process Equipment and Plant Design
The ratio of down take area to cross-sectional area of the tube, for calendria type evaporator ranges from

2 to 2.5
1.5 to 2
1 to 1.5
0.5 to 1

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